US6322351B1 - Burner for use in corrosive atmosphere and process for the combustion of hydrocarbon fuel therein - Google Patents

Burner for use in corrosive atmosphere and process for the combustion of hydrocarbon fuel therein Download PDF

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Publication number
US6322351B1
US6322351B1 US09/393,710 US39371099A US6322351B1 US 6322351 B1 US6322351 B1 US 6322351B1 US 39371099 A US39371099 A US 39371099A US 6322351 B1 US6322351 B1 US 6322351B1
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US
United States
Prior art keywords
burner
steam
hydrocarbon fuel
corrosive atmosphere
combustion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US09/393,710
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English (en)
Inventor
Thomas Sandahl Christensen
Ivar Ivarsen Primdahl
Olav Holm-Christensen
Peter Seier Christensen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Topsoe AS
Original Assignee
Haldor Topsoe AS
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Haldor Topsoe AS filed Critical Haldor Topsoe AS
Priority to US09/393,710 priority Critical patent/US6322351B1/en
Assigned to HALDOR TOPSOE A/S reassignment HALDOR TOPSOE A/S ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CHRISTENSEN, PETER SEIER, CHRISTENSEN, THOMAS SANDAHL, HOLM-CHRISTENSEN, OLAV, PRIMDAHL, IVAR IVARSEN
Application granted granted Critical
Publication of US6322351B1 publication Critical patent/US6322351B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/46—Details, e.g. noise reduction means
    • F23D14/72—Safety devices, e.g. operative in case of failure of gas supply
    • F23D14/76—Protecting flame and burner parts
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/46—Details, e.g. noise reduction means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
    • F23L7/002—Supplying water
    • F23L7/005—Evaporated water; Steam
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D2212/00—Burner material specifications
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D2900/00—Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
    • F23D2900/00018—Means for protecting parts of the burner, e.g. ceramic lining outside of the flame tube
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
    • F23L2900/07002—Injecting inert gas, other than steam or evaporated water, into the combustion chambers

Definitions

  • the present invention is directed to combustion of hydrocarbon fuel in a burner and a device for carrying out the combustion process.
  • Hydrocarbon fuel is in the chemical industry usually used in the firing of industrial furnaces and process heaters and to supply heat to heat requiring reactions proceeding in reaction vessels provided with appropriate burners.
  • a general drawback of the known burners is damage of the burner face at high fuel gas velocities, as required for industrial burners and metal dusting caused by corrosive atmosphere to which the burner's surface is exposed at high temperatures.
  • U.S. Pat. No. 5,496,170 discloses a swirling flow burner with improved design to prevent hot combustion products from internal recycling through a combustion adjacent to the burner face. Thereby, damage of the burner face caused by the hot combustion products is substantially prevented.
  • this invention is a process for the combustion of hydrocarbon fuel in a burner being exposed to corrosive atmosphere, wherein a non-corrosive atmosphere is passed along outer surface of the burner to protect the surface from contact with the corrosive atmosphere.
  • Suitable non-corrosive atmosphere will be any gaseous medium, which does not cause metal dusting or carburization reactions on metallic surfaces at elevated temperature.
  • Suitable non-corrosive atmospheres included steam H 2 , CO 2 and nitrogen or mixtures thereof.
  • the invention provides a burner for the combustion of hydrocarbon fuel with an oxidant comprising within an outer metallic surface passages for supplying fuel and oxidant, and an orifice for combustion of the fuel with the oxidant, the improvement comprising a wall concentrically and spaced apart surrounding at least part of the outer metallic surface of the burner and being adapted to introduce and passing a protective atmosphere along the surface.
  • the wall When operating the above burner in a reactor, the wall may be formed by refractory lining material at top of the reactor surrounding the outer surface of the burner in a suitable distance and, thereby, forming passageway for introduction and passage of the protective atmosphere during operation of the burner.
  • a burner 2 having an outer surface with cylindrical metallic surface 4 and a conical metallic orifice 6 is mounted in top part of a reactor 1 .
  • An annular space 10 between upper surface 4 and part of orifice 6 is formed between the burner surface and a refractory lining 8 in burner 1 .
  • Through annular space 10 steam is passed along upper surface 4 and directed to orifice 6 .
  • the steam being passed through annular space 10 protects the outer surface from corrosive combustion atmosphere and prevents carburization or metal clusting reaction the surface caused by the combustion atmosphere.
  • the critical temperature was found in each test by gradually lowering the exit temperature of the reactor (T Exit ) until the soot limit was surpassed.
  • the value was, furthermore, determined for a burner without a protecting steam flow at otherwise identical conditions i.e. inlet flow, operational pressure and steam carbon ratio.
  • the steam to carbon ratio (S/C) is defined as the sum of all steam feeds in moles divided by the sum of hydrocarbons in moles of carbon atoms (C 1 ).
  • the pilot plant used in the above tests comprises units for providing the different feed streams to the ATR reactor, the ATR reactor and equipment for post treatment of the product gas.
  • the feed streams consisted of natural gas, steam, oxygen and hydrogen. All gases were compressed to operating pressure and preheated to operating temperature.
  • An average composition of the natural gas is given in Table 1.
  • the natural gas was desulphurised before introduction into the ATR reactor.
  • the feed streams were combined into three steams and passed to the burner of the ATR.
  • a first feed stream of natural gas, hydrogen and steam was preheated to a temperature of about 500° C.
  • a second feed stream containing oxygen and steam was preheated to between 200° C. and 220° C.
  • a third feed stream consisting only of steam was heated to 450° C.
  • Metal dusting test are carried out at a steam to carbon ratio (S/C) of 0.60 (MD S/C 0.60) and 0.35 (MD S/C 0.35), respectively.
  • S/C steam to carbon ratio
  • T Inlet,1 and T Inlet,2 are the inlet temperatures of the first and second feed streams, respectively
  • T Exit and P Exit are the temperature and the pressure of the gas leaving the reactor, at which conditions the steam reforming and shift reactions are in equilibrium.
  • the burner is removed from the ATR reactor for inspection. While the burner without protecting steam flow on the outer wall showed region on the surface being corroded by metal dusting on the outside surface of the gas nozzle, the outside nozzle of the burners with protection steam showed no sign of metal dusting on the outer surface.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)
US09/393,710 1998-09-15 1999-09-10 Burner for use in corrosive atmosphere and process for the combustion of hydrocarbon fuel therein Expired - Lifetime US6322351B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US09/393,710 US6322351B1 (en) 1998-09-15 1999-09-10 Burner for use in corrosive atmosphere and process for the combustion of hydrocarbon fuel therein

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10046098P 1998-09-15 1998-09-15
US09/393,710 US6322351B1 (en) 1998-09-15 1999-09-10 Burner for use in corrosive atmosphere and process for the combustion of hydrocarbon fuel therein

Publications (1)

Publication Number Publication Date
US6322351B1 true US6322351B1 (en) 2001-11-27

Family

ID=22279878

Family Applications (1)

Application Number Title Priority Date Filing Date
US09/393,710 Expired - Lifetime US6322351B1 (en) 1998-09-15 1999-09-10 Burner for use in corrosive atmosphere and process for the combustion of hydrocarbon fuel therein

Country Status (12)

Country Link
US (1) US6322351B1 (de)
EP (1) EP0987492B1 (de)
JP (1) JP4179717B2 (de)
KR (1) KR100372826B1 (de)
CN (1) CN1196888C (de)
AU (1) AU755430B2 (de)
CA (1) CA2282014C (de)
DE (1) DE69908267T2 (de)
NO (1) NO318563B1 (de)
NZ (1) NZ337738A (de)
RU (1) RU2249765C2 (de)
TW (1) TW403821B (de)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005017411A1 (de) * 2003-07-18 2005-02-24 Linde Aktiengesellschaft Gasbrenner

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8506660B2 (en) * 2007-09-12 2013-08-13 General Electric Company Nozzles for use with gasifiers and methods of assembling the same

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US733579A (en) * 1903-04-01 1903-07-14 Joseph Fitton Hydrocarbon-burner.
JPS60171310A (ja) * 1984-02-15 1985-09-04 Babcock Hitachi Kk 低ΝＯｘバ−ナ装置
US4986748A (en) * 1989-12-15 1991-01-22 Corning Incorporated Wide range oxy-fuel burner and furnace operation
US5496170A (en) * 1991-12-06 1996-03-05 Haldor Topsoe A/S Swirling-flow burner
US5515794A (en) * 1995-01-23 1996-05-14 Texaco Inc. Partial oxidation process burner with recessed tip and gas blasting
US6193173B1 (en) * 1998-06-15 2001-02-27 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Burner with an improved injector and process for manufacturing this injector

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4125360A (en) * 1976-10-28 1978-11-14 Envirotech Corporation Steam atomizing burner
US5209656A (en) * 1991-08-29 1993-05-11 Praxair Technology, Inc. Combustion system for high velocity gas injection
US5266025A (en) * 1992-05-27 1993-11-30 Praxair Technology, Inc. Composite lance
US5597298A (en) * 1994-12-13 1997-01-28 Praxair Technology, Inc. Laminar flow burner

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US733579A (en) * 1903-04-01 1903-07-14 Joseph Fitton Hydrocarbon-burner.
JPS60171310A (ja) * 1984-02-15 1985-09-04 Babcock Hitachi Kk 低ΝＯｘバ−ナ装置
US4986748A (en) * 1989-12-15 1991-01-22 Corning Incorporated Wide range oxy-fuel burner and furnace operation
US5496170A (en) * 1991-12-06 1996-03-05 Haldor Topsoe A/S Swirling-flow burner
US5515794A (en) * 1995-01-23 1996-05-14 Texaco Inc. Partial oxidation process burner with recessed tip and gas blasting
US6193173B1 (en) * 1998-06-15 2001-02-27 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Burner with an improved injector and process for manufacturing this injector

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005017411A1 (de) * 2003-07-18 2005-02-24 Linde Aktiengesellschaft Gasbrenner
US20070134608A1 (en) * 2003-07-18 2007-06-14 Hanno Tautz Gas burner

Also Published As

Publication number Publication date
NO994449D0 (no) 1999-09-14
CA2282014A1 (en) 2000-03-15
JP4179717B2 (ja) 2008-11-12
AU755430B2 (en) 2002-12-12
NO318563B1 (no) 2005-04-11
NZ337738A (en) 2001-03-30
NO994449L (no) 2000-03-16
KR20000023143A (ko) 2000-04-25
DE69908267D1 (de) 2003-07-03
EP0987492A1 (de) 2000-03-22
CN1249414A (zh) 2000-04-05
CA2282014C (en) 2008-08-26
TW403821B (en) 2000-09-01
RU2249765C2 (ru) 2005-04-10
DE69908267T2 (de) 2004-04-08
EP0987492B1 (de) 2003-05-28
JP2000186806A (ja) 2000-07-04
KR100372826B1 (ko) 2003-02-20
AU4759299A (en) 2000-03-23
CN1196888C (zh) 2005-04-13

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